FR2459680A2 - REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE - Google Patents

REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE Download PDF

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Publication number
FR2459680A2
FR2459680A2 FR8013810A FR8013810A FR2459680A2 FR 2459680 A2 FR2459680 A2 FR 2459680A2 FR 8013810 A FR8013810 A FR 8013810A FR 8013810 A FR8013810 A FR 8013810A FR 2459680 A2 FR2459680 A2 FR 2459680A2
Authority
FR
France
Prior art keywords
reactor
tube
loop reactor
hand
communication
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
FR8013810A
Other languages
French (fr)
Other versions
FR2459680B2 (en
Inventor
Herwig Burgert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BURGERT BURDOSA
Original Assignee
BURGERT BURDOSA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BURGERT BURDOSA filed Critical BURGERT BURDOSA
Publication of FR2459680A2 publication Critical patent/FR2459680A2/en
Application granted granted Critical
Publication of FR2459680B2 publication Critical patent/FR2459680B2/fr
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/04Separating crystals from mother liquor
    • C13B30/14Dissolving or refining raw sugar
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F21/00Dissolving
    • B01F21/20Dissolving using flow mixing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/435Mixing tubes composed of concentric tubular members
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • B01F25/51Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/833Flow control by valves, e.g. opening intermittently
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/834Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices the flow of substances to be mixed circulating in a closed circuit, e.g. from a container through valve, driving means, metering means or dispensing means, e.g. 3-way valve, and back to the container
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • B01J19/2435Loop-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/56Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

REACTEUR A BOUCLES POUR REACTIONS CHIMIQUES ET SIMILAIRES. LE REACTEUR A BOUCLES 1 ETANT MONTE HORIZONTALEMENT, UNE TUBULURE DE REMPLISSAGE 8 EST DISPOSEE A LA PARTIE SUPERIEURE DE L'ENVELOPPE ET, EN DEHORS DE L'ENVELOPPE DU REACTEUR, UNE POMPE DE CIRCULATION 11 EST RELIEE AU TUBE DE SORTIE 10, LAQUELLE EST EN COMMUNICATION, PAR L'INTERMEDIAIRE D'UN TUBE 13, D'UNE PART AVEC L'ADMISSION DE LIQUIDE 14 ET, D'AUTRE PART, AVEC LE DISPOSITIF DE SOUTIRAGE 15, 16. UN TEL REACTEUR SE REVELE EFFICACE POUR MELANGER DES SOLIDES AVEC DES LIQUIDES.LOOP REACTOR FOR CHEMICAL AND SIMILAR REACTIONS. THE LOOP REACTOR 1 BEING MOUNTED HORIZONTALLY, A FILLING TUBING 8 IS PROVIDED AT THE UPPER PART OF THE ENCLOSURE AND, OUTSIDE THE REACTOR ENCLOSURE, A CIRCULATION PUMP 11 IS CONNECTED TO THE OUTLET TUBE 10, WHICH IS IN COMMUNICATION, THROUGH A TUBE 13, ON THE ONE HAND WITH THE INLET OF LIQUID 14 AND, ON THE OTHER HAND, WITH THE TAPPING DEVICE 15, 16. SUCH REACTOR IS EFFECTIVE FOR MIXING SOLIDS WITH LIQUIDS.

Description

L'invention est relative à un réacteur à boucles selon le brevet 76 10The invention relates to a loop reactor according to the patent 76 10

888. Des réacteurs de cette structure sont surtout destinés  888. Reactors of this structure are mainly intended for

au mélange des matières liquides.to the mixture of liquid materials.

Les matières solides et liquides,par exemple lors de la prépara-  Solids and liquids, for example during the preparation

tion d'une solution de sucre,sont actuellement mélangées dans un dispositif à agitation, Celui-ci consiste le plus souvent en une cuve dans laquelle tourne un agitateur à hélice. Etant donné que, dans ce casles matières solides sont plaquées sur la paroi de la cuve sous l'effet de la force centrifuge,le processus de mélange est long et n'est pas suffisamment intime. Le contenu de la cuve  Sugar solution is presently mixed in a stirring device. This is usually a vessel in which a propeller stirrer is rotated. Since in this case the solids are plated on the wall of the tank under the effect of the centrifugal force, the mixing process is long and not sufficiently intimate. The contents of the tank

doit être chaque fois vidé et la cuve être rechargée. Le fonction-  must be emptied each time and the tank be recharged. The function

nement discontinu du système d'agitation se traduit,lors de la  discontinuous stirring system is reflected, during the

fabrication,par une perte de temps indésirable.  manufacturing, by an undesirable waste of time.

Le problème à la base de l'invention est de mettre au point un dispositif dans lequel le mélange de matières solides et liquides  The problem underlying the invention is to develop a device in which the mixture of solids and liquids

s'effectue de façon rapide et intense.  is done quickly and intensively.

Dans son principele problème est résolu selon l'invention grâce à l'utilisation d'un réacteur à boucles selon le brevet 76 10 888  In its main problem is solved according to the invention through the use of a loop reactor according to the patent 76 10 888

qui s'est déjà révélé extrêmement efficace pour le mélange de matiè-  already proven to be extremely effective for the blending of

res liquides. Pour le mélange des matières solides avec des liquides, l'invention fournit un réacteur à boucles comportant une enveloppe de réacteur cylindrique,un tube directeur disposé concentriquement à celleci et muni d'un anneau creux qui est en communicationd'une part,avec l'enceinte de mélange par une ouverture dans l'enveloppe externe du tube directeur et, d'autre part,avec le tube de sortie du réacteur par au moins une autre ouverture à l'extrémité du tube directeur,une admission de liquide disposée concentriquement à l'extrémité opposée du tube directeur et des moyens pour le brassage du liquide selon le brevet 75 10 888,qui présente la particularité  liquids. For the mixing of solids with liquids, the invention provides a loop reactor having a cylindrical reactor shell, a steering tube concentrically disposed thereto and provided with a hollow ring which is in communication with both mixing chamber through an opening in the outer casing of the head tube and, secondly, with the reactor outlet tube through at least one other opening at the end of the head tube, a liquid inlet arranged concentrically to the opposite end of the steering tube and means for mixing the liquid according to the patent 75 10 888, which has the particularity

que le réacteur à boucles,étant monté horizontalement,une tubu-  that the loop reactor, being mounted horizontally, a tubular

lure de remplissage est disposée à la partie supérieure de l'en-  The filling lure is arranged at the top of the enclosure.

veloppe et que,en dehors de l'enveloppe du réacteur,une pompe de  veloppe and that, outside the reactor casing, a fuel pump

circulation est reliée au tube de sortielaquelle est en communica-  circulation is connected to the output tube which is in communication with

tion,par l'intermédiaire d'un tube,d'une part avec l'admission de  tion, through a tube, on the one hand with the admission of

liquide et, d'autre part,avec le dispositif de soutirage. De préfé-  liquid and, on the other hand, with the withdrawal device. Preferably

rence,sur la tubulure de remplissage est disposé un indicateur de niveau asservi au dispositif de soutirage. L'invention fournit aussi un procédé de mélange de matières solides avec des liquides qui comporte l'emploi d'un tel réacteur  A filling level indicator is provided on the filler neck which is controlled by the draw-off device. The invention also provides a method for mixing solids with liquids which involves the use of such a reactor

à boucles,et selon lequel,de préférence,les matières sont introdui-  loops, and according to which, preferably, the materials are introduced

tes en contiru dans le mélange en circulation dans l'enveloppe de réacteur remplie et le mélange est soutiré par pompage,est en partie  Contoured in the circulating mixture in the filled reactor casing and the mixture is pumped off, is partly

injecté dans le corps du réacteur et est en partie soutiré.  injected into the reactor body and is partially withdrawn.

L'utilisation du réacteur à boucles selon l'invention offre également l'avantage que les matières solides et liquides peuvent  The use of the loop reactor according to the invention also has the advantage that solid and liquid materials can

être amenées en continu dans la cuve à réaction.  be fed continuously into the reaction vessel.

Le dessin représente une vue latérale,partiellement en coupe,  The drawing shows a side view, partially in section,

d'un exemple de réalisation d'un réacteur à boucles selon l'inven-  of an embodiment of a loop reactor according to the invention.

tion.tion.

Dans la cuve à réaction cylindrique 1 est logé concentrique-  In the cylindrical reaction vessel 1 is housed concentrically

ment le tube directeur 2 qui,sur une partie de sa longueur à double paroi, est constitué par un anneau creux 5 avec une paroi externe 3 et une paroi interne 4,L'extrémité de la paroi externe forme avec la paroi interne une ouverture 6. A l'autre extrémité du tube directeurdes tubes 7 conduisent vers la sortie 10. Sur le bord supérieur de la cuve est disposée une tubulure de remplissage 8, de préférence pour les matières solides,dans laquelle débouche un tube 9 pour liquides. La pompe de circulation 11 également zur la face supérieure de la cuve est en communication avec la sortie 10 par le tube d'aspiration 12 et avec la buse d'injection 14 et la cuve 1 par l'intermédiaire du tube sous pression 13. Le tube de sortie 15,dans lequel est insérée une soupape de réglage 16 couplée à un indicateur de niveau 17 placé dans la tubulure de remplissage 8,est placé en dérivation par rapport au tube sous pression 13,  the steering tube 2 which, over part of its double-walled length, is constituted by a hollow ring 5 with an outer wall 3 and an inner wall 4, the end of the outer wall forms with the inner wall an opening 6 At the other end of the tube directing tubes 7 lead to the outlet 10. On the upper edge of the tank is arranged a filling pipe 8, preferably for solids, in which opens a tube 9 for liquids. The circulation pump 11 also on the upper face of the tank is in communication with the outlet 10 via the suction tube 12 and with the injection nozzle 14 and the tank 1 via the pressure tube 13. outlet tube 15, in which is inserted a control valve 16 coupled to a level indicator 17 placed in the filler neck 8, is placed in connection with the pressure tube 13,

Un robinet 18 est destiné à la vidange de la cuve.  A valve 18 is intended for emptying the tank.

Le réacteur une fois rempli,la pompe de circulation 11 assure une circulation intense de la quantité de matière chargée à travers le  Once the reactor has been filled, the circulation pump 11 ensures an intense circulation of the quantity of material charged through the

réacteur et par conséquent un mélange intime. Aussitôt que le pro-  reactor and therefore an intimate mixture. As soon as the

duit fini est soutiré à travers la soupape 16,on règle l'indica-  finished product is withdrawn through the valve 16, the indica-

teur de niveau 17 de manière que les produits à mélanger soient  level 17 so that the products to be blended are

délivrés vers le réacteur en une quantité correspondant au soutira-  delivered to the reactor in an amount corresponding to the

ge du produit fini.ge of the finished product.

Claims (3)

REVENDICATIONS 1. Réacteur à boucles comportant une enveloppe de réacteur cylindrique,un tube directeur disposé concentriquement à celle-ci et muni d'un anneau creux qui est en communication,d'une part, avec l'enceinte de mélange par une ouverture dans l'enveloppe externe du tube directeur et, d'autre partavec le tube de sortie du réacteur par au moins une autre ouverture à l'extrémité du tube directeur,une admission de liquide disposée concentriquement à l'extrémité opposée du tube directeur et des moyens pour le brassage du liquide selon le brevet 75 10 888,caractérisé en ce que, le réacteur à boucles (1) étant monté horizontalement,une tubulure de remplissage (8)est disposée à la partie supérieure de l'nveloppe  1. Loop reactor comprising a cylindrical reactor shell, a steering tube concentrically disposed thereon and provided with a hollow ring which is in communication, on the one hand, with the mixing chamber by an opening in the outer casing of the director tube and, on the other handwith the reactor outlet tube by at least one other opening at the end of the director tube, a liquid inlet arranged concentrically at the opposite end of the director tube and means for the stirring of the liquid according to the patent 75 10 888, characterized in that, the loop reactor (1) being mounted horizontally, a filler neck (8) is arranged at the upper part of the nipple et que,en dehors de l'enveloppe du réacteur,une pompe de circula-  and that, outside the reactor casing, a circulation pump tion (11) est reliée au tube de sortie (10),laquelle est en communication, par l'intermédiaire d'un tube (13),d'une part avec l'admission de liquide (14)et, d'autre partavec le dispositif de soutirage (15,16)o  tion (11) is connected to the outlet tube (10), which is in communication, via a tube (13), on the one hand with the liquid inlet (14) and on the other hand with the withdrawal device (15, 16) o 2. Réacteur à boucles selon la revendication l,caractérisé en ce que sur la tubulure de remplissage (8) est disposé un indicateur2. loop reactor according to claim 1, characterized in that on the filler pipe (8) is arranged an indicator de niveau (17)asservi au dispositif de soutirage (15,16).  level (17) slaved to the withdrawal device (15, 16). 3. Utilisation du réacteur à boucles selon la revendication 1 ou  3. Use of the loop reactor according to claim 1 or 2 pour le mélange de matières solides avec des liquides.  2 for mixing solids with liquids. Procédé de mélange selon la revendication 3,caractérisé en ce que les matières sont introduites en continu dans le mélange en circulation dans l'enveloppe de réacteur remplie et que le mélange  Mixing process according to Claim 3, characterized in that the substances are introduced continuously into the circulating mixture in the filled reactor casing and that the mixture est soutiré par pompage,est en partie injecté dans Ze corps du réac-  is pumped off, is partly injected into the body of the reaction teur et est en partie soutiré.and is partly withdrawn.
FR8013810A 1979-06-22 1980-06-20 REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE Granted FR2459680A2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2925191A DE2925191C2 (en) 1979-06-22 1979-06-22 Loop reactor

Publications (2)

Publication Number Publication Date
FR2459680A2 true FR2459680A2 (en) 1981-01-16
FR2459680B2 FR2459680B2 (en) 1985-04-26

Family

ID=6073861

Family Applications (1)

Application Number Title Priority Date Filing Date
FR8013810A Granted FR2459680A2 (en) 1979-06-22 1980-06-20 REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE

Country Status (10)

Country Link
US (1) US4448539A (en)
JP (1) JPS602905B2 (en)
AT (1) AT376910B (en)
BR (1) BR8003877A (en)
CH (1) CH650942A5 (en)
DE (1) DE2925191C2 (en)
FR (1) FR2459680A2 (en)
GB (1) GB2055050B (en)
IT (1) IT1147752B (en)
NL (1) NL8003552A (en)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4490049A (en) * 1983-06-02 1984-12-25 Cron Chemical Corporation Mixing arrangement
US4701055A (en) * 1986-02-07 1987-10-20 Fluid Dynamics, Inc. Mixing apparatus
JPH01145301U (en) * 1988-03-22 1989-10-05
CH682460A5 (en) * 1990-11-19 1993-09-30 Miteco Ag Angelo Cadeo Apparatus for dissolving solid bulk material in a liquid.
GB9101967D0 (en) * 1991-01-30 1991-03-13 Atomic Energy Authority Uk Reagent mixing
IT1253330B (en) * 1991-07-11 1995-07-24 Agristrade Srl PHYSICAL DISSOLUTOR
US5248416A (en) * 1991-11-18 1993-09-28 Howard Jr Ronnie E Sewage treatment system
US5350595A (en) * 1992-05-13 1994-09-27 Kraft General Foods, Inc. Method for continuous manufacture of process cheese-type products
EP0598283B1 (en) * 1992-11-16 1997-10-29 Bayer Ag Continuous process for the conversion control of polyurethane prepolymers by partially mixing the prepolymers with monomers
US5333952A (en) * 1993-08-17 1994-08-02 Perdue John L Chemical mixing chamber
CA2224033A1 (en) * 1996-12-13 1998-06-13 Kraft Foods, Inc. Method for continuous manufacture of viscous food products
US6239235B1 (en) * 1997-07-15 2001-05-29 Phillips Petroleum Company High solids slurry polymerization
ZA991026B (en) * 1998-02-13 2000-08-10 Coca Cola Co Continuous dry parts metering and blending system.
JP3741253B2 (en) * 1999-12-24 2006-02-01 富士通株式会社 Chemical manufacturing equipment
US6566460B1 (en) 2000-08-04 2003-05-20 Equistar Chemicals, Lp Continuous recovery of polymer from a slurry loop reactor
ES2291668T3 (en) * 2002-09-23 2008-03-01 Total Petrochemicals Research Feluy SUSPENSION LOOP POLYOLEFIN REACTOR.
ES2416314T3 (en) 2004-08-27 2013-07-31 Chevron Phillips Chemical Company Lp Polyolefin production processes
US7629421B2 (en) * 2005-12-21 2009-12-08 Chevron Phillips Chemical Company Lp Monomer recovery by returning column overhead liquid to the reactor
US20090154288A1 (en) * 2007-12-13 2009-06-18 Heathman James F On-the-Fly Acid Blender with High-Rate, Single Pass, Emulsification Equipment
PL2593943T3 (en) * 2010-07-15 2015-03-31 Mallinckrodt Nuclear Medicine Llc Slurry dispenser for radioisotope production
CN104196514B (en) * 2014-09-02 2016-09-14 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 A kind of acidizing and fracturing fluid is i.e. joined and is i.e. used device
US10252229B2 (en) * 2017-06-30 2019-04-09 Snowie LLC System comprising a pump attached to a tank casing for mixing a fluid
BR102017019628B1 (en) * 2017-09-14 2022-03-29 Petrobras Transporte S/A - Transpetro External fluid movement system in a storage tank

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2699379A (en) * 1949-04-22 1955-01-11 Luque Jose Aramburu Extraction apparatus
FR1427464A (en) * 1964-03-20 1966-02-04 Guenter Strumann Method and apparatus for dissolving in water or mixing with water aggressive solid or liquid detergents
US4007921A (en) * 1976-01-19 1977-02-15 The Dow Chemical Company Apparatus for mixing dry particles with a liquid

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA130831A (en) * 1910-10-12 1911-01-31 William C. Paterson Pulp agitating apparatus
US2635859A (en) * 1950-06-12 1953-04-21 Felix W Dreyfus Mixer apparatus
US3166020A (en) * 1961-09-20 1965-01-19 Hypro Engineering Inc Venturi mixer nozzle
US3608869A (en) * 1969-05-28 1971-09-28 Texaco Inc System for blending liquid ingredients
DE2232341A1 (en) * 1972-07-01 1974-01-17 Orthmann & Herbst Continuous neutralization plant - for acid or alkaline waste water
US3807700A (en) * 1972-07-05 1974-04-30 S Kennedy Mixing apparatus for forming a slurry
DE2516284C3 (en) * 1975-04-14 1978-04-13 Burdosa, Herwig Burgert, 6301 Roedgen Loop reactor
US4170420A (en) * 1976-09-13 1979-10-09 Underwood Gene E Fluid mixing system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2699379A (en) * 1949-04-22 1955-01-11 Luque Jose Aramburu Extraction apparatus
FR1427464A (en) * 1964-03-20 1966-02-04 Guenter Strumann Method and apparatus for dissolving in water or mixing with water aggressive solid or liquid detergents
US4007921A (en) * 1976-01-19 1977-02-15 The Dow Chemical Company Apparatus for mixing dry particles with a liquid

Also Published As

Publication number Publication date
IT1147752B (en) 1986-11-26
GB2055050B (en) 1982-12-01
US4448539A (en) 1984-05-15
JPS602905B2 (en) 1985-01-24
GB2055050A (en) 1981-02-25
IT8067971A0 (en) 1980-06-20
ATA323280A (en) 1984-06-15
DE2925191C2 (en) 1982-11-11
DE2925191A1 (en) 1981-03-12
FR2459680B2 (en) 1985-04-26
NL8003552A (en) 1980-12-24
CH650942A5 (en) 1985-08-30
JPS5626541A (en) 1981-03-14
AT376910B (en) 1985-01-25
BR8003877A (en) 1981-01-13

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